CN111408156A

CN111408156A - Hole layout of vapor-liquid contact tray

Info

Publication number: CN111408156A
Application number: CN202010086615.6A
Authority: CN
Inventors: M.W.皮林; S.格吕尔; P.威尔金森; R.E.安德森
Original assignee: Sulzer Chemtech AG
Current assignee: Sulzer Management AG
Priority date: 2014-12-23
Filing date: 2015-06-09
Publication date: 2020-07-14
Anticipated expiration: 2035-06-09
Also published as: BR112017013741A2; CN111408156B; US20180008904A1; EP3434345A1; JP2019162631A; KR20170098261A; MX2017008494A; US10737196B2; EP3218077A1; CN107257703A; RU2681025C2; CN107257703B; JP6777636B2; JP6893601B2; EP3434345B1; JP6780056B2; ES2823485T3; US10596483B2; RU2017126130A; JP2020073277A

Abstract

A vapor-liquid contact tray apparatus includes a tray having a plurality of apertures through which fluid passes. The apertures are arranged in a first set of three adjacent columns extending substantially parallel to the main liquid flow path of the tray. The holes of the middle column are offset from the adjacent holes of the other two columns along the main liquid flow path on the disc to form a triangular pattern of adjacent holes across the three adjacent columns. The apertures have lengths and widths, each length oriented substantially parallel to its column and each width oriented substantially perpendicular to its column. The centers of adjacent apertures within each column are spaced apart by a first spacing equal to or between 2.5 and 4.5 times the average length of the apertures in the column. Adjacent columns are spaced apart by a second spacing equal to or between 1.5 and 2.5 times the average width of the apertures of the adjacent columns.

Description

Hole layout of vapor-liquid contact tray

Background

Mass transfer columns such as distillation, absorption and stripping columns have been provided with various types of trays for vapor-liquid contacting purposes. These columns are well known in the art for separating a multi-component feed stream and are not particularly limited herein. Examples of such towers and trays are described in U.S. patent nos. 4,750,975, 5,120,474, 5,453,222 and 8,066,264, which are incorporated herein by reference.

Typically, mass transfer columns have multiple trays supported horizontally in a spaced configuration over the height of the column. A typical tray has a plate with liquid passing from an inlet downcomer section to an outlet downcomer. Typical tray plates have holes through which rising vapor can flow and over and/or around which liquid can flow to bubble or otherwise force the vapor through the liquid in a cross-flow manner.

The design of a distillation column and its associated trays is a balance between overall material throughput (e.g., capacity) and tray/column separation efficiency. It is therefore an object of the present invention to increase the capacity of trays and columns, or in the alternative, to increase efficiency, without sacrificing performance.

The selection and placement of the holes of the disc is guided in part by the principles described above. However, the vapor and/or liquid interaction between adjacent pores on the disc and the impact on efficiency and capacity are not fully understood. U.S. patents 5,468,425 and 5,975,504, which are incorporated herein by reference in their entirety for all purposes, describe hole layouts and "desired" hole spacing for optimal performance of vapor-liquid contact trays. These patents show a triangular pattern of holes across several columns of holes on the disk and describe the spacing between holes in a desired column and the spacing between columns. However, these patents do not provide a proper understanding of the interaction between adjacent holes on the disc, and as a result, the "required" spacing between holes does not provide optimal disc performance (e.g., capacity and/or efficiency). Therefore, it is highly desirable to obtain a better understanding of these interactions and to provide a layout and spacing of the holes that enhances the performance of the disc.

It is also noted that the trays are supported within the tower by the underlying tray supports. The layer tray support may interact with holes in the tray to provide dead space areas on the tray where vapor/liquid interaction is reduced. Therefore, it is strongly desired to better understand these dead spaces on the disc and to provide a way to increase the vapor/liquid interaction therein to improve the performance of the disc.

Disclosure of Invention

In a first aspect, the present invention provides a vapour-liquid contact disc arrangement comprising a disc having a plurality of apertures for passage of fluid through the disc, wherein:

the apertures are arranged in a first set of three adjacent columns extending substantially parallel to the main liquid flow path of the tray,

the apertures of the middle column are offset from adjacent apertures of the other two columns along the main liquid flow path on the disc to form a triangular pattern of adjacent apertures across the three adjacent columns,

the apertures have a length and a width, each length oriented along its column, and each width oriented substantially perpendicular to its column,

the centers of adjacent holes within each column are spaced apart by a first spacing equal to or between 2.5 and 4.5 times the average length of the holes in the column, and

adjacent columns are spaced apart by a second spacing equal to or between 1.5 and 2.5 times the average width of the apertures of the adjacent columns.

In a second aspect, the present invention provides another vapor-liquid contact tray apparatus for use in a separation column. The apparatus comprises a tray and a tray support, wherein:

the disc support comprises one or more elements selected from the group consisting of: a ring, partial ring, bracket or flange underlying and supporting a circumferential region of the disk; a cross member located below and supporting a chord region of the disc; and a tray panel forming a cross beam supporting a portion of an adjacent one or more tray panels of the tray;

a plurality of support region vents formed in the tray laterally adjacent the tray support;

one or more of the plurality of support area vents are at least partially covered by a cover positioned to interact with steam passing through the support area vents such that greater than 50% of the steam passing through the support area vents is directed laterally across the tray and over an underlying tray support.

In a third aspect of the invention, another vapor-liquid contact tray apparatus for use in a separation column is provided. The apparatus comprises all the elements of the first and second aspects of the invention.

In a fourth aspect, the present invention provides a fractionation column comprising one or more vapor-liquid contacting trays as outlined in any of the above aspects of the invention.

In a fifth aspect, the present invention provides a method of producing a top stream and a bottom stream from one or more feed streams. The method comprises the following steps:

(i) introducing one or more feed streams to a mass transfer column according to the fourth aspect of the invention, an

(ii) The mass transfer column is treated under operating conditions sufficient to produce a top stream and a bottom stream,

thereby, a top stream and a bottom stream are generated from the one or more feed streams.

Drawings

Fig. 1 is a top view of a disk apparatus (tray apparatus) according to the present invention.

Fig. 2 is a top view of a disk apparatus according to the present invention.

Fig. 3 is a perspective view of a ladder valve.

Fig. 4 and 5 show graphical results from an exemplary section.

Fig. 6-10 are side cross-sectional views of disk devices according to the present invention.

Detailed Description

The present description is based, in part, on the inventors' first discovery of the layout and configuration of the holes separating the disks, which improves the performance of the disks (e.g., increases capacity while maintaining or improving efficiency). The present description is also based in part on the inventors' second discovery of the arrangement and configuration of the holes separating the trays, which provides for venting of the portion of the trays directly above the underlying tray support, which also improves the performance of the trays. Although the first and second findings of the present inventors may be used alone to improve the performance of a disc, it is believed that using a combination of both the first and second findings together in the same disc may have cumulative benefits.

I. Layout of the holes:

a first finding of the present inventors is that the lateral steam flows leaving adjacent orifices and valves can impinge on each other, creating a region of high steam momentum that limits the capacity of the disc. The inventors have surprisingly found that the configuration of the orifices and valves of the disc of the present invention minimizes and/or eliminates this shock effect. In particular, the present inventors have discovered a hole layout for a mass transfer column tray (mass transfer column) that increases the tray capacity while maintaining or improving the separation efficiency of the tray. In a preferred embodiment, the spacing between the pores is a function of the average size of the pores. In other preferred embodiments, the spacing between the holes is a function of the type of hole. Mass transfer columns containing one or more trays of the present invention can achieve higher capacity and equal or higher separation efficiency than columns of similar size and design that do not employ trays of the present invention.

Referring to fig. 1, a vapor-liquid contact tray assembly 100 includes a tray 101 having a plurality of apertures 103 for fluid flow through the tray 101. In some embodiments, the tray 101 includes separate panels (not shown) that can be secured to one another to form the tray 101 (e.g., a tray deck).

The apertures 103 are arranged in a first set of three adjacent columns of

apertures

107, 109, 111 extending substantially parallel to the main liquid flow path 113 of the tray 101. The main liquid flow path 113 extends between an inlet downcomer section 114 and an outlet downcomer section 116 of the tray 101. In practice, the "main liquid flow path" 113 is the general direction of liquid flow over the disc between the inlet downcomer section 114 and the outlet downcomer section 116, although there may be micro-scale or regional liquid flow paths on the disc 101 caused by the interaction of the liquid, vapor, their associated general and/or regional velocities, and/or characteristics of the disc 101. In certain embodiments, the tray may have more than one inlet downcomer section 114 and/or more than one outlet downcomer section 116. In these embodiments, the tray may have more than one main liquid flow path 113, each of which extends between a respective inlet downcomer section 114 and a respective outlet downcomer section 116.

As described above, the disk apertures 103 are arranged in a first set of three adjacent columns of

apertures

107, 109, 111 extending substantially parallel to the main liquid flow path 113 of the disk 101. The term "substantially parallel" is understood herein to mean that the respective one or more rows of apertures 103 are positioned at about-15 ° to +15 ° relative to the main liquid flow path 113 of the tray, e.g., the respective one or more rows of apertures 103 are positioned at about-10 ° to +10 ° relative to the main liquid flow path 113 of the tray (e.g., about-5 ° to +5 °, about-2 ° to +2 °, or parallel (e.g., about 0 °)).

The apertures 103 of the middle column 109 are offset from adjacent apertures 103 of the other two

adjacent columns

107, 111 on the disk 101 along the main liquid flow path 113 to form a triangular pattern 115 of adjacent apertures 103 across the three

adjacent columns

107, 109, 111.

Turning to fig. 2 (e.g., a close-up view of the hole layout on the disk), the holes 203 have a length 217 and a width 219. Each length 217 is oriented substantially parallel to (e.g., on or along) its

column

207, 209, 211, the

columns

207, 209, 211 being substantially parallel to the main liquid flow path 213 on the tray 201. Each width 219 is oriented substantially perpendicular to its

columns

207, 209, 211 (e.g., substantially perpendicular to the main liquid flow path 213 on the tray 201). Similar to the above, the term "substantially" throughout this application and is understood herein to mean within about-15 ° to +15 °, within about-10 ° to +10 °, within about-5 ° to +5 °, more preferably between about-2 ° to +2 °, or about 0 ° relative to a reference direction (e.g., parallel or perpendicular).

The centers of adjacent apertures 203 within each

column

207, 209, 211 are spaced apart by a first spacing 221, the first spacing 221 being equal to or between 2.5 and 4.5 times the average length 217 of the apertures 203 in the

column

207, 209, 211. In a more preferred embodiment, the centers of adjacent apertures 203 within each

column

207, 209, 211 are spaced apart by a first spacing 221, the first spacing 221 being equal to or between 2.9 and 3.9 times, such as between 3.5 and 3.7 times (e.g., 3.6 times) the average length 217 of the apertures 203 in the

column

207, 209, 211.

Centerlines 223 of

adjacent columns

207, 209, 211 are spaced at a second spacing 225, the second spacing 225 being equal to or between 1.5 and 2.5 times an average width 219 of apertures 203 of

adjacent columns

207, 209, 211. In a more preferred embodiment, centerlines 223 of

adjacent columns

207, 209, 211 are spaced at a second spacing 225, the second spacing 225 being equal to or between 1.7 and 2.2 times, such as between 1.9 and 2.1 times (e.g., 2.0 times) the average width 219 of apertures 203 of

adjacent columns

207, 209, 211.

In a preferred embodiment, the centers of adjacent apertures 203 in each

column

207, 209, 211 are spaced apart by a first spacing 221, the first spacing 221 being greater than 76mm, e.g., equal to or between about 95-130 mm. Further, in the preferred embodiments, centerlines 223 of

adjacent columns

207, 209, 211 are spaced at a second spacing 225, the second spacing 225 being equal to or less than 40mm, such as equal to or between about 30-38 mm. In these preferred embodiments, the average length of the apertures is preferably equal to or between about 17mm and 52mm (e.g., equal to or between about 30-48mm, and more preferably equal to or between 40-47 mm), and/or the average width of the apertures is preferably equal to or between about 10mm and 26mm (e.g., equal to or between about 10-20 mm).

In other preferred embodiments, there is no overlap of apertures 203 between

adjacent columns

207, 209, 211 along the main liquid flow path 213 of the disk. In other words, any line drawn perpendicular to the main liquid flow path 213 and through any two adjacent columns of apertures in the first set of three adjacent columns intersects at most one aperture 203 of that two adjacent columns.

In other preferred embodiments, in addition to the first set of three adjacent columns, the other apertures of the plurality of apertures are arranged in one or more additional sets of three adjacent columns extending parallel to the main liquid flow path of the tray (shown in fig. 1). For example, a tray may have 3, 4, 5, 6, 7,8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20 or more rows of holes extending parallel to the main

liquid flow paths

113, 213 on the tray. The grouping of three adjacent columns may include a common column between the groupings. For example, a disk with four columns of holes may be considered to have two sets of three adjacent columns (e.g.,

columns

1, 2, and 3 and/or columns 2, 3, and 4), and so on.

Where the disc has one or more further groups of three adjacent columns of apertures, it is preferred that the groups have similar or identical characteristics to the first group. In particular, it is preferred that the apertures of the middle column of the one or more further groups are offset from adjacent apertures of the other two columns of the groups along the main liquid flow path on the disc to form a triangular pattern of adjacent apertures across the adjacent three columns of the one or more further groups. Further, the apertures in the one or more additional groups have a length and a width, each length oriented along its column and each width oriented perpendicular to its column. It is also preferred that the centres of adjacent holes within each column of the one or more further groups are spaced apart by a first spacing equal to or between 2.5 and 4.5 times the average length of the holes in that column, and adjacent columns of the one or more further groups are spaced apart by a second spacing equal to or between 1.5 and 2.5 times the average width of the holes in that adjacent column.

The holes in the tray provide flow paths for vapor to pass upwardly through the tray and through liquid traveling along the main liquid flow path of the tray. The size and shape of the disc holes are not particularly limited.

In certain embodiments, the length of the aperture is positioned along or substantially parallel to the main liquid flow path on the tray, while the width is positioned along or substantially perpendicular to the main liquid flow path. The average length of the holes is preferably equal to or between about 10mm and about 70mm (e.g., equal to or between about 17mm and about 52mm, equal to or between about 30-48mm, more preferably equal to or between 40-47mm, e.g., 45 mm). In these embodiments, the average width of the apertures is preferably equal to or between about 5mm and about 40mm (e.g., equal to or between about 10mm and about 26mm, equal to or between about 10-20mm, such as 19 mm).

In other preferred embodiments, the apertures will have a shape selected from the group consisting of: circular, square, rectangular, trapezoidal, pentagonal, and hexagonal. In other preferred embodiments, one or more or all of the apertures are trapezoidal and positioned such that their parallel sides are substantially perpendicular to the main liquid flow path of the tray (e.g., wherein the longer parallel side is upstream of the shorter parallel side along the main liquid flow path). Since the trapezoidal shaped holes have a long width upstream and a short width downstream along the main liquid flow path on the tray, the average width of the trapezoidal shaped holes can be used to determine their placement on the tray.

In other preferred embodiments, one or more or all of the apertures are rectangular and positioned such that their long parallel sides are substantially parallel to the main liquid flow path and their short parallel sides are substantially perpendicular to the main liquid flow path. The size and shape of the apertures may also preferably be selected to control and/or minimize liquid flow through the tray deck (e.g., to allow liquid to leak from the main liquid flow path of the tray through the tray to a lower position in the column/tower).

The aperture may be associated with a cover that at least partially covers the aperture. Where an orifice cover is present, it is preferably selected to control leakage, vapor flow rate, vapor direction, liquid flow rate and direction, and/or the introduction/distribution of vapor or contact with liquid traveling along the main liquid flow path of the tray.

Orifice covers are well known in the art and are not particularly limited herein. In a preferred embodiment, there are one or more orifice covers that at least partially cover one or more orifices (e.g., all of the orifices of the tray). The aperture and its associated cover, if present, are referred to in the art as a "valve" and the cover may be inserted into and/or associated with the aperture after aperture formation or, in the alternative, formed from a disc plate (e.g., by stamping and/or bending) when the aperture is formed. These valves may be fixed valves whose covers remain fixed relative to the tray deck, or floating valves whose covers variably open and close relative to the tray deck depending on vapor flow rate and liquid level.

Non-limiting examples of valves are described in U.S. Pat. Nos. 7,540,476, 7,708,258, 8,066,264 and 8,720,870, which are incorporated herein by reference for all purposes.

When one or more fixed valves are present, they are preferably trapezoidal valves and are punched out by the disc plate, and their length is oriented parallel to the liquid flow. Trapezoidal valves offer unique advantages over other types of valves or uncovered holes (e.g., sieve trays). In particular, they allow for lower foam height, less entrainment due to lateral steam release (entrainment), increased capacity, improved regulation (turndown), high efficiency over a wider operating range by improved vapor-liquid contact, excellent mechanical strength by increasing the stiffness of the disc plate, no moving parts and therefore no wear and excellent fouling resistance. Some of the ladder valves are shown in figure 3.

When one or more float valves are present, they preferably comprise movable or float valves that maximize hydraulic capacity, separation efficiency and operating range of the fractionation trays. The main characteristics of these valves include an umbrella or concave shaped cover to reduce the ejection momentum of the released vapor, minimize entrained vapor-liquid entrainment, promote uniform mixing of the vapor and liquid on the tray deck, and maximize the contact area of the vapor and liquid on the tray deck. Two wide legs movably secure this type of valve to the disk plate and serve to maximize robustness against rotation, wear, and valve ejection from the disk plate, and maximize run length and minimize maintenance costs. In addition, four spacers are included to prevent adhesion to the tray deck and maximize scale prevention. Two thicknesses and lifts are provided to maximize flexibility and operating range. The orientation of the valve is parallel to the liquid flow, which serves to minimize the hydraulic gradient with the flow path of the disc plate.

It is also noted that fixed or movable valves with umbrella or concave covers can produce further desired vapor flow profiles. For example, an umbrella or concave shaped cap may be used to direct steam away from the holes in an outward but downward vector (toward the tray deck). For example, steam exiting the apertures interacts with a concave or umbrella-shaped cover and is redirected radially outward away from the apertures and then back away from the apertures toward the tray deck (e.g., back toward the tray deck and away from the apertures at an oblique angle). The flow of steam generated by these types of valves allows the momentum of the steam exiting the valve to carry the steam outwardly away from the valve and downwardly (e.g., back toward the disk plate and away from the orifice at an oblique angle) through the liquid traveling along the disk plate. Without being limited by a particular operating mechanism, this is believed to allow greater venting of liquid and the ability to vent a larger area of the disc with these types of valves.

Aeration of the liquid flow on the tray directly above the tray support and support:

the trays are typically supported within the tower by tray supports that are secured to the tower and underlie the trays and support one or more of the trays and/or their respective panels. The area of the disk directly overlying the disk support typically has no holes, and therefore, the liquid flow path above the disk support is typically not vented. In the alternative, these areas of the disk do have holes, but the steam flow through the holes is blocked by the underlying disk supports. In either case, these areas, i.e., the non-vented areas, are generally considered to be "dead" (e.g., non-vented) areas.

The inventors have found that when these normally non-vented regions of the disc are vented, the pressure drop across the disc can be reduced/minimized while increasing the capacity of the disc. Accordingly, in another aspect of the present invention, the disk apparatus described herein may further include: a disk support, wherein the disk is supported by the disk support; and structure (e.g., means for the purpose) that enables venting of at least a portion of the main liquid flow path directly above the disk support. Where these structures are employed for venting at least a portion of the main liquid flow path directly above the disk support, it is preferred that they are sufficient to vent a portion (e.g., 25% or more, 50% or more, 75% or more, or all) of the liquid flow path directly above the disk support.

Disc supports and their associated elements are well known in the art and are not particularly limited herein. For example, the disc support and its associated elements may comprise, among others: a ring, partial ring, bracket and/or flange secured to the tower underlying and supporting a circumferential area of the disk; a beam (e.g., a truss system) secured to the tower, which underlies and supports the chordal region of the disc; and/or an integrated truss system that utilizes one or more tray panels to support other panels of a tray (e.g., a tray panel that forms a cross beam that underlies and supports a portion of an adjacent one or more tray panels); and combinations thereof.

The structure that enables venting of at least a portion of the main liquid flow path directly above the disk support is also not particularly limited. In certain embodiments, the structure comprises an element/feature associated with the tray that comprises a support-area aperture (vent) formed in the tray directly above the tray support.

In embodiments where the tray comprises a support region vent formed in the tray directly above the tray support, a corresponding element/feature is preferably associated with the tray support that allows fluid communication from below the tray and through the support region vent above the tray support. In one embodiment, the corresponding elements/features associated with the disk support include an aperture in the disk support that is in fluid communication with a support area vent in the disk directly above the disk support. United states patents 2,274,041, 2,903,251, 4,174,363, US 5,547,617 and 7,810,796, incorporated herein for all purposes, describe additional corresponding elements/features associated with the tray support that allow fluid communication from below the tray through the support area vents above the tray support. For example, U.S. patent 7,810,796 describes the use of spacers disposed between the tray and the tray support. In these embodiments, the spacers serve to lift the tray from the support, allowing fluid communication from below the tray through support area vents disposed directly above the tray support. These patents also describe embodiments incorporated herein for all purposes that provide aeration to liquid on the tray directly above the tray support.

In yet additional embodiments, partially the subject of the inventors' second discovery and illustrated in fig. 6-10, the structure capable of venting at least a portion of the liquid 602 directly above the tray support 604 comprises one or more support-area vents 603 formed in the tray 601 and positioned (e.g., laterally, radially, or horizontally) adjacent to the underlying tray support 604. As shown in fig. 6, support area vents 603 are preferably located within about 5mm, within about 2.5mm, within about 1.5mm, or less of, i.e., adjacent to, the chassis support 604. As described herein, embodiments of the second discovery of the present inventors may be used alone or in combination with the embodiments of the first discovery of the present inventors described above. However, it is believed that using a combination of both the first and second findings together in the same disc may have a cumulative benefit in improving the performance of the disc.

Where support area vents 603 are employed laterally adjacent to a tray support, it deflects steam 606 laterally outward (e.g., radially or horizontally) along the tray deck to adjacent tray supports 604 or directly above adjacent tray supports 604. A portion of the exiting vapor 606 travels within the liquid 602 in the direction of the bottom tray support 604 and to a location above the bottom tray support 604, thereby venting at least a portion of the liquid 602 directly above the tray support 604. In other embodiments, apertures 603 are associated with a fixed or floating cover to help direct steam further laterally outward across the tray deck. In a preferred embodiment, and as described above, the fixed or floating cover will have an umbrella or concave shape that can produce a further desired steam flow distribution. For example, an umbrella or concave shaped cap may be used to direct steam away from the holes in an outward but downward vector (toward the tray deck). For example, steam exiting the support area vents interacts with a concave or umbrella-shaped cover and is redirected radially outward away from the apertures and then back away from the apertures toward the tray deck (e.g., back toward the tray deck and away from the apertures at an oblique angle). The flow of steam generated by these types of valves allows the momentum of the steam exiting the valve to carry the steam outwardly away from the valve and downwardly (e.g., back toward the tray deck at an oblique angle and away from the support area apertures) through the liquid traveling along the tray deck. Without being limited by a particular operating mechanism, this is believed to allow greater aeration of the liquid above the disk support and the ability to aerate a greater area above the support.

In other preferred embodiments, the flow of steam 606 exiting the support area vents 603 is biased in the direction of and above the adjacent tray supports 604. In these embodiments, it is preferred that greater than 50% (e.g., greater than 75% or all) of the steam passing through the support area vents is deflected in the direction of and to a position overlying the adjacent sub-tray support.

The structure (e.g., means for the above purpose) that is capable of deflecting greater than 50% of the steam 606 flowing through the support area vents exiting the support area vents 603 is not particularly limited herein. However, these structures preferably include an orifice cover associated with the orifice 603. In a preferred embodiment, the aperture cover has one or more openings positioned to direct greater than 50% of the steam passing through the support area vents in the direction of and to a position overlying an adjacent chassis support. The lid may optionally have additional openings positioned to direct steam over other portions of the tray not directly above the tray support. The covers may be fixed relative to the disk such that the openings are fixed in an open position, or they may be floating valves having a variable height relative to the disk plate during operation of the disk.

As shown in fig. 7, in one embodiment, it is contemplated that a fixed "push" cover 708 (e.g., a "push" valve) may be employed to bias the flow of steam 706 from the support area vents 603 over the bottom tray support 704. Fixed push caps or push valves are known in the art and are commonly used in separation trays to facilitate movement of liquid over the trays along the main liquid flow path of the trays (e.g., from an inlet downcomer section to an outlet downcomer section). In other words, a push valve as used in the art includes an orifice cover having a single opening that biases vapor in the direction of (e.g., parallel to) the main liquid flow path on the tray. Typically, the push valve is formed integrally with the disc at the time of hole formation, wherein a slit is formed in the disc and the slit is subsequently deformed to provide an opening in the disc directed in the direction of the main liquid flow path.

In the current embodiment, the use of a push valve to bias the steam flow above the underlying tray support is counterintuitive and contrary to how push valves are employed in the art. For example, where the support region vents 603 are positioned laterally adjacent to the underlying tray support ring and/or chordal tray support having cross-beams/struts that are substantially parallel to the main liquid flow path of the tray, employing a push valve associated with the support region vents 603 will cause the steam flow to be biased in a different direction from the main liquid flow path on the tray (e.g., in a direction that is not parallel to the main liquid flow path on the tray). For example, in these embodiments, the vapor may be biased at or between 10 and 170 degrees relative to the main liquid flow path of the tray (e.g., perpendicular to the main liquid flow path of the tray or at an oblique angle relative to the main liquid flow path of the tray).

The hole cover used to support the area vent 603 may also be a floating cover. In these embodiments, the lid is openable and closable such that the height of the lid and its corresponding opening can vary relative to the tray deck depending on the vapor flow rate through the support area vent, the liquid level on the tray, or both the vapor flow rate through the support area vent and the liquid level on the tray.

As shown in fig. 8, the inventors have discovered a particularly preferred floating cover 808 for use with support area vents 803. The cover 808 includes a concave top cover 810, one or more legs 812, and one or more feet 814. When the cover 808 is associated with the support area vents 803, the concave top cover 810 faces the tray 801 and at least partially covers the support area vents 803. One or more legs 812 are connected to the top cover 810 and disposed through the support area vents 803. One or more feet 814 are provided beneath the disk 801 and interact with the underside of the disk 801 to prevent the cover 808 from being removed from the disk 801 after its initial insertion. When the cover 808 is moved from the closed position to the open position, the legs 812 move within and interact with the support area vents 803 as the top cover 810 moves away from the tray 801. As the top cover 808 moves away from the tray 801, it tilts to an oblique angle relative to the tray 801, thereby exposing an opening that points in the direction of the underlying tray support 804. As top cover 810 moves further away from disk plate 801, the opening pointing in the direction of the adjacent bottom disk support 804 becomes larger, thereby biasing more steam flow 806 in the direction of disk support 804 and to a position above disk support 804. The top cover 810 may continue to move away from the tray 801 and may preferably continue to tilt until the feet 814 disposed below the tray 801 become engaged with the underside of the tray 801 when the cover 808 is in the fully open or fully tilted position.

Similar to the discussion above regarding the use of a fixed or floating valve with an umbrella or concave top cover, the use of an umbrella or concave top cover with the present tilt valve can produce a preferred vapor flow profile that biases vapor above the adjacent bottom disk support. Here, the steam flow interacts with the cover to lift the cover from the tray deck. When steam interacts with the umbrella or concave roof, the direction of the steam flow shifts from vertically away from the tray deck to horizontally along the tray deck and above the adjacent supports. In certain embodiments, an umbrella or concave top cover may be provided such that some steam is redirected back toward the tray deck at an oblique angle away from the respective support area vent holes, but still in the direction of the adjacent base tray area support. In other embodiments, a portion (e.g., less than 50%) of the vapor allowed to pass through the support region vents may pass through other apertures in the cover 808, which does not result in venting of liquid above adjacent tray supports.

The inclination of the cover 808 is preferably provided by the physical interaction between the legs 812 of the cover 808 and the support area vents 803 of the tray 801. In this embodiment, and as shown in fig. 9 and 10 (which respectively show the valve in the closed and open positions), between the

caps

910, 1010 and one or more of the

feet

914, 1014, the

legs

912, 1012 may be tapered (as shown in fig. 9) or rocked (as shown in fig. 10). For example, where the legs 912 are tapered or have tapered portions, the legs 912 have a greater width positioned toward the top cover 910 as compared to a lesser width positioned toward the one or more feet 914. This feature allows the legs 912 to interact with the holes 903 when the lid 908 is open and allows the top cover 910 to tilt relative to the tray 901 when the lid 908 is open. In another example where the leg 1012 is rocking or has a rocking portion, the leg 1012 may have a constant width between the top cover and one or more feet 1014. In this embodiment, the legs 1012 have an arcuate shape or are otherwise rocking, wherein the interaction between the rocking/arcuate legs and the support area vents 1003 allow the lid to tilt relative to the tray when the lid is opened. Also, in these embodiments, the canopy actively biases the steam flow 1006 toward and into a position above the laterally adjacent bottom tray support 1004.

Further, as shown in fig. 9, one or more of the legs 912 and/or one or more of the feet 914 may have a structure such as a flange, bump, or protrusion 918 that may further interact with the underside of the tray 901 to resist removal of the cover 908 after it is inserted into the aperture 903. As a final step in the assembly of the cover, a flange, bump or protrusion 918 may be provided after inserting legs 912 and feet 914 through apertures 903. In some embodiments, when the cover 908 has more than one leg 912 (e.g., two legs 912) and/or more than one foot 914 (e.g., two feet 914), a corresponding ledge, bump, or protrusion 918 may be formed on only one of the legs 912 or only one of the feet 914. In this embodiment, the respective leg and/or foot will be asymmetric with the other of the legs and/or feet and will further prevent the cover 908 from being removed after insertion into the aperture 903. This feature will also facilitate manufacture and/or assembly of the tray, as a corresponding flange, bump or protrusion 918 may be used to guide proper alignment of the cover 908 in a corresponding hole, such that the cover 908 is tilted in the proper direction (e.g., away from the underlying support 904) to ensure proper biasing of the steam over the underlying support. In other embodiments, the following structures (e.g., bumps, flanges, protrusions, etc.) are formed in the cover prior to insertion into the aperture: this structure may resist removal of cover 908 after cover 908 is inserted into the hole. In this embodiment, the legs may be sufficiently resilient to allow slight bending of the legs for insertion into the holes and passage of structures (e.g., bumps, flanges, protrusions, etc.), and then, to allow the legs to return to their original shape after insertion.

Mass transfer columns and methods of operation:

the contact tray apparatus of the present invention is intended for use in mass transfer columns. Accordingly, in another aspect, the present invention provides a mass transfer column comprising one or more contact disc apparatus according to any of the embodiments described herein.

The trays are arranged horizontally in a spaced configuration along the height of the column such that liquid enters the trays at the inlet downcomer section from higher in the column and exits the trays at their outlet downcomer to a lower location in the column. In a preferred embodiment, the column will have a plurality of horizontally disposed contact trays, wherein 5% or more, 15% or more, 25% or more, 50% or more, 75% or more, or all of the trays within the column comprise tray devices according to any of the embodiments described herein.

In another embodiment, an existing conventional mass transfer column can be modified to include one or more disk devices according to any of the embodiments described herein. A decision to retrofit an existing tower can be made to increase the capacity of the tower without incurring the cost of design and replacement of the entire tower.

The present invention also provides a method of generating a top stream (overhead stream) and a bottom stream from one or more feed streams. Other streams, such as byproduct streams or secondary feed streams, may be provided to or removed from the column. The method includes a first step of introducing one or more feed streams to a mass transfer column having horizontally disposed tray apparatus according to any of the embodiments described herein. The second step comprises: the one or more feed streams are treated under operating conditions within the column sufficient to produce a top stream and a bottom stream. The operation of the mass transfer column is well known in the art, and the operating conditions are not particularly limited. In another embodiment, the horizontally disposed tray arrangement includes one or more support area vents positioned laterally adjacent to the underlying tray support. In this further embodiment, the method may further comprise the steps of: greater than 50% of the steam directed through the support area vents laterally across the tray and to a location above the tray support.

Increase in disk capacity and efficiency and decrease in steam side pressure drop across the disk:

the inventors have found that it is possible to increase the operating capacity of the disc while maintaining or improving the efficiency of the disc and while maintaining or reducing the pressure drop across the disc. These characteristics can be achieved by employing the following: the layout of the holes described herein; the manner of venting the liquid flow path of the tray above the tray support described herein; or a combination of both.

In some embodiments, the operational capacity of the disc may be increased by 5% or more, 10% or more, 15% or more, or 20% or more as compared to a disc that does not include these features. In other embodiments, the operational capacity of the disc is increased by 5% to 25% without reducing the efficiency of the disc.

In still other embodiments, the vapor side pressure drop across the disc may be reduced by 5% or more, 10% or more, 15% or more, or 20% or more without reducing the efficiency of the disc as compared to a disc without these features. In other embodiments, the vapor side pressure drop across the disk is reduced by 5% to 25% without reducing the efficiency of the disk.

In yet further embodiments, as the gas load of the disk increases, the disk of the present invention exhibits an increase in separation efficiency of the disk of 5% or more, 10% or more, 15% or more, or 20% or more, as compared to a disk not having these features.

Reference throughout the specification to "one embodiment," "another embodiment," "an embodiment," "some embodiments," and so forth, means that a particular element (e.g., feature, structure, attribute, and/or characteristic) described in connection with the embodiment is included in at least one embodiment described herein, and may or may not be present in other embodiments. In addition, it is to be understood that the described elements may be combined in any suitable manner with any other elements of the embodiments.

V. example:

having described the invention in detail, the following examples are provided. These examples should not be considered as limiting the scope of the invention, but merely as being illustrative and representative thereof.

Three discs (e.g. plates) with different hole configurations and optionally means for venting the liquid flow path above the disc support were investigated under the same conditions in the test setup (base line Deck), plate I and plate II). The baseboard is considered herein as a comparative example, while the boards I and II are considered within the scope of the invention.

Baseboard is a common commercial recommendation based on the arrangement of holes on a board (e.g., the commercial standard that existed prior to the present invention). The base plate has a plurality of holes for fluid to pass through the disk. The apertures are arranged in a first set of three adjacent columns extending parallel to the main liquid flow path of the disk. The middle column of apertures is offset from the adjacent apertures of the other two columns along the main liquid flow path on the disk to form a triangular pattern of adjacent apertures across the adjacent three columns. The apertures have lengths and widths, each length oriented along its column and each width oriented perpendicular to its column. The centers of adjacent apertures within each column are spaced apart by a first spacing that is less than 2.5 times the average length of the apertures in the column. Adjacent columns are spaced apart by a second spacing that is greater than 2.5 times the average width of the apertures of adjacent columns. The base plate is supported by the disk support and no venting means is provided to vent the liquid flow path on the plate directly above the disk support.

Board I is similar to a baseboard. A first difference between the board I and the base board is that the centres of adjacent holes within each column are spaced by a first spacing equal to or between 2.5 and 4.5 times the average length of the holes in the column. A second difference between the board I and the base board is that adjacent columns are spaced apart by a second spacing equal to or between 1.5 and 2.5 times the average width of the holes of adjacent columns. Like the base plate, plate I is supported by the disk support and no venting means is provided to vent the liquid flow path on the plate directly above the disk support.

Board II is similar to board I and contains the same differences as board I compared to the baseline board. However, plate II includes another difference in that plate II is supported by a supporting disk ring having holes in fluid communication with holes in the disk overlying the ring. This fluid communication allows venting of the liquid flow path on the plate directly above the disc support. It is also noted that in further testing with the disc in direct contact with the support ring, similar results were obtained to those of plate II, however, a tilted valve was placed in the disc adjacent (e.g., radially/laterally) to the support ring to direct and disperse the vapor radially outward (e.g., radially) over the ring to vent the liquid flow path on the disc above the ring.

The results of the graphical test of the four discs described above with respect to each other are plotted in fig. 4 and 5. As can be seen in fig. 4 and 5, the trays of the present invention (plate I and plate II) show improved capacity, sustained and/or reduced vapor side pressure loss, and sustained and/or increased tray separation efficiency compared to the baseline board.

Claims

1. A vapor-liquid contact tray apparatus for use in a separation column, the apparatus comprising a tray and a tray support, wherein:

2. The apparatus of claim 1, wherein the height of the lid relative to the tray deck is variable depending on the vapor flow rate through the support area vent holes, the liquid level on the tray, or both the vapor flow rate through the support area vent holes and the liquid level on the tray.

3. The apparatus of claim 1 or 2, wherein the cover comprises a top cover disposed over the tray and at least partially covering the support area vent, the top cover being connected to one or more legs disposed through the support area vent, and the one or more legs being provided with one or more feet disposed below the tray, wherein the feet interact with an underside of the tray to prevent removal of the cover from the tray.

4. The apparatus of claim 3, wherein the legs:

is vertically movable within the support area vent to allow for variation in the height of the top cover from the tray deck, an

Tapering or rocking between the foot and the top cover to allow the top cover to tilt relative to the tray deck as the leg moves within the aperture.